WO1999023128A1 - Catalyst and method for trimerization of isocyanates - Google Patents
Catalyst and method for trimerization of isocyanates Download PDFInfo
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- WO1999023128A1 WO1999023128A1 PCT/FR1998/002359 FR9802359W WO9923128A1 WO 1999023128 A1 WO1999023128 A1 WO 1999023128A1 FR 9802359 W FR9802359 W FR 9802359W WO 9923128 A1 WO9923128 A1 WO 9923128A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/30—Low-molecular-weight compounds
- C08G18/38—Low-molecular-weight compounds having heteroatoms other than oxygen
- C08G18/3819—Low-molecular-weight compounds having heteroatoms other than oxygen having nitrogen
- C08G18/3842—Low-molecular-weight compounds having heteroatoms other than oxygen having nitrogen containing heterocyclic rings having at least one nitrogen atom in the ring
- C08G18/3848—Low-molecular-weight compounds having heteroatoms other than oxygen having nitrogen containing heterocyclic rings having at least one nitrogen atom in the ring containing two nitrogen atoms in the ring
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/02—Polymeric products of isocyanates or isothiocyanates of isocyanates or isothiocyanates only
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/0234—Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
- B01J31/0235—Nitrogen containing compounds
- B01J31/0239—Quaternary ammonium compounds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/0234—Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
- B01J31/0235—Nitrogen containing compounds
- B01J31/0244—Nitrogen containing compounds with nitrogen contained as ring member in aromatic compounds or moieties, e.g. pyridine
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/0234—Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
- B01J31/0255—Phosphorus containing compounds
- B01J31/0267—Phosphines or phosphonium compounds, i.e. phosphorus bonded to at least one carbon atom, including e.g. sp2-hybridised phosphorus compounds such as phosphabenzene, the other atoms bonded to phosphorus being either carbon or hydrogen
- B01J31/0268—Phosphonium compounds, i.e. phosphine with an additional hydrogen or carbon atom bonded to phosphorous so as to result in a formal positive charge on phosphorous
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/02—Polymeric products of isocyanates or isothiocyanates of isocyanates or isothiocyanates only
- C08G18/022—Polymeric products of isocyanates or isothiocyanates of isocyanates or isothiocyanates only the polymeric products containing isocyanurate groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/16—Catalysts
- C08G18/18—Catalysts containing secondary or tertiary amines or salts thereof
- C08G18/1875—Catalysts containing secondary or tertiary amines or salts thereof containing ammonium salts or mixtures of secondary of tertiary amines and acids
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/16—Catalysts
- C08G18/18—Catalysts containing secondary or tertiary amines or salts thereof
- C08G18/20—Heterocyclic amines; Salts thereof
- C08G18/2009—Heterocyclic amines; Salts thereof containing one heterocyclic ring
- C08G18/2027—Heterocyclic amines; Salts thereof containing one heterocyclic ring having two nitrogen atoms in the ring
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
- C08L75/04—Polyurethanes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/30—Addition reactions at carbon centres, i.e. to either C-C or C-X multiple bonds
- B01J2231/34—Other additions, e.g. Monsanto-type carbonylations, addition to 1,2-C=X or 1,2-C-X triplebonds, additions to 1,4-C=C-C=X or 1,4-C=-C-X triple bonds with X, e.g. O, S, NH/N
- B01J2231/341—1,2-additions, e.g. aldol or Knoevenagel condensations
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2115/00—Oligomerisation
- C08G2115/02—Oligomerisation to isocyanurate groups
Definitions
- the subject of the invention is a catalyst useful for the catalytic cyclotrimerization of monomeric isocyanates to polyisocyanates.
- EP-003 765 describes the partial cyclotrimerization of isophorone diisocyanate (IPDI or 1 -isocyanato-3,3,5-trimethyl-5-isocyanatomethyl-cyclohexane) using as a catalyst a hydroxide of a hydroxyalkylammonium quaternary.
- catalysts based on a quaternary ammonium hydroxide have a very strong reactivity which makes it difficult to control the trimerization reaction, in particular when the starting isocyanate is an aliphatic or cycloaliphatic isocyanate.
- the hydrolysable chlorine content also influences the coloration of the reaction crude which increases as the quantity of chlorine is high.
- US 4,040,992 further describes catalysts for the catalytic trimerization of isocyanates of the quaternary ammonium salt type, the anion of which is represented by OH " , or the formula OOC- (O) a -Y in which Y is chosen from: an atom hydrogen, an alkyl group having from 1 to 20 carbon atoms, an alkenyl group having from 2 to 15 carbon atoms, a cycloalkyl group having from 3 to 6 carbon atoms, a phenyl group, an alkylphenyl group having from 1 to 9 carbon atoms in the alkyl radical or in the groups linked to the phenyl ring, a benzyl group, a carbamate group, a group alkylbenzyl having from 1 to 9 carbon atoms in the alkyl residue or in the groups linked to the benzyl ring, and a group CH (3.
- Z is (CH 2 ) d COOR in which d is an integer from 0 to 4 and R is a hydrogen atom or an alkyl group having up to 20 carbon atoms, and a is zero or 1
- anions illustrated in this patent are all anions derived from alkylcarboxylic acid.
- the catalysts described in this document do not make it possible to achieve the desired goal.
- the object of the invention is to provide a catalyst for cyclotrimerization of isocyanates, in particular dnsocyanates which allows control of the reaction, while having an acceptable conversion rate, which is not substantially dependent on the chlorine content. hydrolyzable, starting isocyanate and making it possible to obtain a product whose coloring is not marked markedly.
- the aim of the invention is also to propose a process for the catalytic trimerization of isocyanates, in particular for cyclotimerization partial dnsocyanates, which is easy to control, does not depend or little depends on the content of hydrolyzable chlorine present in the isocyanate monomer and which reduces as much as possible the coloration of the reaction crude
- ionic type catalysts the counter anion of which is the hydrogen carbonate anion, would make it possible to achieve the desired goal.
- These catalysts are formed from a bulky mono-atomic or poly-atomic cation, either as such or in the form of a complex formed with a complexing agent, in particular of the encryption type.
- a subject of the invention is thus the use as a catalyst for the cyclotrimerization reaction of isocyanates of a hydrogen carbonate of a cation which, either as such, or in form complexed with a complexing agent, has an ionic radius or average molecular greater than 1 ⁇ , preferably greater than 1.5 ⁇ , as defined in the tables of M. Shannon and Prewitt in Acta Cris, 1969, vol. B25, page 925 and which is at least partially soluble in the reaction medium.
- the cation is chosen from cations of bulky alkali metals, in particular rubidium and cesium.
- the cation can also consist of a cation of light alkali metal, in complexed form. Mention may in particular be made of the sodium and potassium cations complexed with crown ether.
- the cation can also consist of a molecular species, in which all the atoms are linked by covalent bonds.
- onium type cations the representative species of which are phosphoniums, sulfoniums and quaternary ammoniums.
- Q represents a nitrogen, phosphorus or sulfur atom
- Ri, R 2 , R 3 and R 4 identical or different, denote alkyl groups, optionally hydroxylated, having 1 to 20 carbon atoms, cycloalkyl radicals having from 4 to 15 carbon atoms, optionally substituted with hydroxyl groups, radicals aralkyl having 7 to 15 carbon atoms, optionally substituted with hydroxyl groups or aryl radicals having 6 to 15 carbon atoms, optionally substituted with hydroxyl groups or when Q is N
- two of the residues Ri, R 2 , R 3 or R 4 may also form, with the nitrogen atom and, where appropriate, with a hetero atom, in particular of oxygen or nitrogen, a heterocyclic ring having 4 to 6 carbon atoms, or else when Q is N
- the residues Ri, R 2 and R 3 each represent ethylene residues which form, in association with the quaternary nitrogen atom and another tertiary nitrogen atom, a bicyclic triethylened
- R 5 , Re and R 7, which are identical or different, represent hydrogen, an OH group, an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group having 5 to 7 carbon atoms, an alkenyl group having from 2 to 15 carbon atoms, an alkynyl group having 3 to 6 carbon atoms, a hydroxyalkyl group having 1 to 9 carbon atoms, an aralkyl group having 7 to 10 carbon atoms, an aryl group having 6 to 10 atoms of carbon or a group R 8 -0- (CH 2 ) n in which R 8 is hydrogen, an alkyl residue having from 1 to 12 carbon atoms, a cycloalkyl residue having from 4 to 10 carbon atoms, a residue aralkyl having 7 to 10 carbon atoms or an aryl residue having 6 to 10 carbon atoms; and n is an integer ranging from 1 to 6; R 7 can also also represent an OCOR 9 group, R9 being a C
- Ri, R 2 and R 3 represent identical or different radicals and denote alkyl groups, optionally hydroxylated, having 1 to 20 carbon atoms, cycloalkyl radicals having 4 to 15 carbon atoms, optionally substituted with hydroxyl groups, aralkyl radicals having 7 to 15 carbon atoms, optionally substituted with hydroxyl groups or aryl radicals having 6 to 15 carbon atoms, optionally substituted with hydroxyl groups, two of the residues Ri, R 2 or R 3 can also form with l nitrogen and, where appropriate, with an oxygen hetero atom or another nitrogen hetero atom a heterocyclic ring having 4 to 6 carbon atoms, or else the residues R 1 ( R 2 and R 3 representing each of the ethylene residues which form, in association with the quaternary nitrogen atom and another tertiary nitrogen atom, a bicyclic triethylenediamine skeleton,
- R 5 , R 6 and R 7, which are identical or different, represent hydrogen, an OH group, an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group having 5 to 7 carbon atoms, an alkenyl group having from 2 to 15 carbon atoms, an alkynyl group having 3 to 6 carbon atoms, a hydroxyalkyl group having 1 to 9 carbon atoms, an aralkyl group having 7 to 10 carbon atoms, an aryl group having 6 to 10 carbon atoms carbon or a group R 8 -0- (CH 2 ) n in which R 8 is hydrogen, an alkyl residue having from 1 to 12 carbon atoms, a cycloalkyl residue having from 4 to 10 carbon atoms, an aralkyl residue having from 7 to 10 carbon atoms or an aryl residue having from 6 to 10 carbon atoms; and n is an integer ranging from 1 to 6; R 7 can also represent a group OCORg, R 9 being a
- a group of preferred quaternary ammonium cations consists of the compounds in which: - Ri, R 2 and R 3 identical or different represent a linear C ⁇ -C 4 alkyl group, preferably C1-C3 alkyl, more particularly alkyl in C ⁇ -C 2 , and preferably methyl,
- - R 5 represents H, OH, the methyl group or the hydroxymethyl group
- - R 6 represents H, OH, the methyl group or the hydroxymethyl group
- R 7 represents H, OH, the methyl group, the hydroxymethyl group or the acetyl group
- R 2 and R 3 identical or different represent a C ⁇ -C 4 alkyl group, preferably C 1 -C 3 alkyl, more particularly C -C 2 alkyl, and preferably methyl,
- - R 5 represents H or a C ⁇ -C 4 alkyl group
- - R 6 represents H, OH or a C ⁇ -C 4 alkyl group
- R 7 represents H, OH, alkyl dC 4 or acetyl. without the total of the carbon atoms from ⁇ to R 7 exceeding 8, preferably 6. More advantageously still, the quaternary ammonium cations are preferred in which at least one, preferably two and more preferably the three groups of R ⁇ to R 3 represent the methyl group, R 5 , R 6 and R 7 being as defined above, and preferably only one of R 5 to R 7 being OH.
- R to R 3 are alkyl, C ⁇ -C 4, a hydroxyalkyl group C ⁇ -C 4, and R 5 to R 7 represent H or OH, said compounds advantageously comprising a single OH group in an omega position relative to the central nitrogen atom.
- a more particularly preferred catalyst is choline hydrogenocarbonate, in particular when the isocyanate which it is desired to cyclotimerize is a cycloaliphatic diisocyanate, such as NBDI, IPDI or H ⁇ 2 MDI, or a mixture of a cycloaliphatic diisocyanate as previously mentioned and of a straight chain or branched chain aliphatic diisocyanate, in particular HDI.
- a cycloaliphatic diisocyanate such as NBDI, IPDI or H ⁇ 2 MDI
- the catalysts according to the invention are known compounds. They can be obtained in particular in the case of quaternary ammoniums, when R represents OH by reaction of a tertiary amine of general formula II:
- the hydroxylated quaternary ammonium can be esterified using an acylimidazole by example.
- ethers we will work with an excess of epoxy.
- the catalyst according to the invention can be used for the cyclotrimerization of any type of isocyanates, or mixture of isocyanates whether they are aliphatic, cycloaliphatic or aromatic, including the prepolymers having terminal isocyanate groups, in particular those described in US 5,115,071 the content of which is incorporated by reference in the present application.
- IPDI isophorone diisocyanate or 1-isocyanato-3,3,5-trimethyl-5-isocyanato methyl cyclohexane
- NBDI nonorbomane diisocyanate or 2,5 (6) -diisocyanato-methyl -bicyclo [2,2,1] heptane
- H ⁇ 2 MDI 4,4'-diisocyanate- dicyclohexylmethanediyl
- HDI hexamethylene diisocyanate
- the catalyst according to the invention is added in an amount between 300 and 5000 ppm, preferably between 500 and 3500 ppm relative to the total amount of the starting isocyanates.
- the catalyst is added to the reaction medium with stirring, preferably in the absence of solvent.
- the reaction is allowed to proceed for a period varying between 1 h and 4 h, preferably approximately one and a half hours.
- the reaction is advantageously carried out at a temperature between room temperature and 120 ° C, preferably between 40 and
- the invention also relates to the use of the catalyst in a solid form such as for example obtained by deposition of the catalyst on a mineral such as silica, or by covalent fixing on a resin.
- the invention also relates to a process for catalytic trimerization of isocyanates, in particular diisocyanates or of a mixture isocyanates, in particular diisocyanates, characterized in that a quaternary ammonium hydrogenocarbonate as defined above is used as the trimerization catalyst.
- cyclotrimerization reaction can be improved substantially when using imidazole or one of its derivatives as a co-catalyst of a catalytic system based on a quaternary ammonium salt.
- the invention therefore also relates to a process for the preparation of isocyanurate polyisocyanates by catalytic cyclotrimerization of isocyanates in which a catalytic system is used comprising as catalyst a cyclotrimerization catalyst based on a quaternary ammonium salt and as co -catalyst imidazole or one of its derivatives.
- imidazole derivatives means any compound comprising the imidazole ring and carrying one or more substituents customary in organic chemistry.
- the imidazole derivatives correspond in particular to the general formula I:
- R ,, R 2 and R 3, which are identical or different, are chosen from H, OH, SH, a C 1 -C alkyl group, C 1 -C 4 hydroxyalkyl, C 1 -C 4 aminoalkyl, C 1 -C C alkylamino, dialkylamino ( each alkyl group having from 1 to 4 carbon atoms), C ⁇ -C 4 alkylthio, C1-C4 haloalkyl, C 3 -Cs cycloalkyl, C 5 -C ⁇ 0 aryl, (C 5 -C 10 aryl) ; - d-C alkyl; (dC alkyl), - C5-C10 aryl, heterocyclic in which the heterocycle comprises from 2 to 10 carbon atoms and from 1 to 4 identical heteroatoms or different chosen from 0, S and N and the group NR, R 4 being in particular C ⁇ -C alkyl or C 3 -C 8 cycloalkyl and n is equal to
- the catalyst based on a quaternary ammonium salt is as defined above.
- any type of known cyclotrimerization catalyst of the quaternary ammonium salt type can be used.
- Ri, R 2 and R 3 represent identical or different radicals and denote alkyl groups, optionally hydroxylated, having 1 to 20 carbon atoms, cycloalkyl radicals having 4 to 15 carbon atoms, optionally substituted with hydroxyl groups, aralkyl radicals having 7 to 15 carbon atoms, optionally substituted with hydroxyl groups or aryl radicals having 6 to 15 carbon atoms, optionally substituted with hydroxyl groups, two of the radicals R ⁇ R 2 or R 3 can also form with l nitrogen and, where appropriate, with an oxygen hetero atom or another nitrogen hetero atom a heterocyclic ring having 4 to 6 carbon atoms, or else the residues R ⁇ R 2 and R 3 representing each of the ethylene residues which form, in association with the quaternary nitrogen atom and another tertiary nitrogen atom, a bicyclic triethylenediamine skeleton,
- R and R 5 which are identical or different, represent hydrogen and / or an alkyl group having 1 to 12 carbon atoms, a cycloalkyl group having 5 to 7 carbon atoms, an alkenyl group having 2 to 15 carbon atoms an alkynyl group having 3 to 6 carbon atoms, a hydroxyalkyl group having 1 to 9 carbon atoms, an aralkyl group having 7 to 10 carbon atoms, an aryl group having 6 to 10 carbon atoms or a group R 6 -0- (CH 2 ) n in which R 6 is hydrogen, an alkyl residue having from 1 to 12 carbon atoms, a cycloalkyl residue having from 4 to 10 carbon atoms, an aralkyl residue having from 7 to 10 carbon atoms or an aryl residue having 6 to 10 carbon atoms; and n is an integer having a value from 1 to 6; and
- X " represents an anion, advantageously chosen from OH " , and the anions of formula ' OOC- (O) a -Y in which Y is chosen from a hydrogen atom, an alkyl group having from 1 to 20 carbon atoms, an alkenyl group having from 2 to 15 carbon atoms, a cycloalkyl group having from 3 to 6 carbon atoms, a phenyl group, an alkylphenyl group having from 1 to 9 carbon atoms in the alkyl residue or in the groups linked to the nucleus phenyl, a benzyl group, a carbamate group, an alkylbenzyl group having from 1 to 9 carbon atoms in the alkyl radical or in the groups linked to the benzyl ring, and a CH (3-b ) Z ( b) group in which b is an integer of 1 to 3 and Z is OH, CN, Cl, an aikoxy group of 1 to 5 carbon atoms, or a
- R is a hydrogen atom or an alkyl group having up to 20 carbon atoms; and a is equal to zero or 1.
- X preferably represents the carboxylate anions and the HCO 3 " anion.
- the isocyanate which it is desired to cyclotimerize is a cycloaliphatic diisocyanate, such as NBDI, IPDI or H 12 MDI, or a mixture of a cycloaliphatic diisocyanate and an aliphatic diisocyanate with a straight chain, in particular HDI , it is preferable to use as catalyst a hydrogenocarbonate of a quaternary ammonium, as defined above, in particular choline hydrogen carbonate.
- catalytic system comprising a quaternary ammonium salt and imidazole or derivatives, in accordance with the present invention, makes it possible to achieve an increase in the reactivity of isocyanates, in particular cycloaliphatic isocyanates, the where appropriate, in admixture with straight chain aliphatic isocyanates, which reactivity can be effectively controlled without depending substantially on the hydrolyzable chlorine content of the starting monomeric isocyanate (s) .
- the reaction mixture obtained at the end of the cyclotrimerization reaction exhibits a strongly attenuated coloring compared to a reaction mixture obtained in the absence of imidazole.
- the use of imidazole as a co-catalyst of a cyclotrimerization reaction in which the catalyst is a quaternary ammonium salt results in the formation of a substantial amount of dimers with a uretdione ring of (s ) (l ') isocyanate (s) starting, capable of improving the properties of the resulting mixture, in particular to reduce the viscosity of polyisocyanates isocyanurates.
- the imidazole is added with stirring to the isocyanate monomer (s) which it is desired to polymerize, preferably in the absence of solvent, and the stirring is continued until a homogeneous mixture is obtained.
- the catalyst is added while stirring is maintained and the reaction medium is heated.
- the reaction is allowed to proceed for a period varying between 1 h and 4 h, preferably approximately 1 hour and a half.
- imidazole as a co-catalyst also makes it possible to substantially reduce the amount of catalyst necessary for the cyclotrimerization of (is) (is) isocyanate (s).
- an amount of catalyst ranging from 100 to 300 ppm, preferably about 200 ppm, relative to the amount of starting isocyanate (s), when the amount of cocatalyst is 400 to 800 ppm, preferably around 600 ppm, based on the amount of starting isocyanate (s).
- the cyclotrimerization reaction in particular partial cyclotrimerization reaction is carried out at a temperature between room temperature and 120 ° C, advantageously from 60 to 70 ° C for IPDI.
- the subject of the invention is also a polyisocyanate (poly) isocyanurate composition obtained by the process according to the invention, in particular comprising the following compounds:
- HDI the proportion of HDI can vary from 5 to 95% by weight.
- the subject of the invention is also a composition of polyisocyanates (poly) isocyanurates obtained by the process according to the invention, such a composition being characterized by the presence of reaction products between the starting isocyanate and the imidazole and between the products for the polymerization of these isocyanates, in particular in the form of isocyanurates with imidazole or one of its derivatives, these products possibly also comprising biuret, carbamate and / or allophanate groups obtained by reaction of the isocyanate groups with the OH groups present in the catalyst .
- the products obtained can subsequently undergo a chemical reaction: dimerization, allophanation, biuretization, blocking reaction with a blocking (or masking) agent either before or after distillation of the monomer.
- the compounds obtained are used for the preparation of coatings, in particular as basic constituents for varnishes and paints.
- IPDT isophorone diisocyanate trimer
- IPDT 80 g of IPDT are obtained, corresponding to a conversion rate of 10%.
- choline hydrogen carbonate has also been compared to that of choline hydroxide, choline bisulfite and choline bitartrate.
- the IPDI (800 g) is loaded into a reactor of 11, and stirred under a stream of argon.
- Imidazole is introduced at a rate of 4 mmol / 100 g of IPDI at room temperature. Stirring is maintained and the reaction medium is brought to 80 ° C. When the temperature has stabilized, choline bicarbonate (0.05% by weight) is introduced. The evolution of the reaction is followed by measuring the transformation rate (TT) of the IPDI of time by measuring the titer in NCO (potentiometry). 99/23128
- the reaction is continued for a period of 1 hour 30 minutes.
- the conversion rate of the IPDI obtained is of the order of 70%.
- the reaction is continued at 80 ° C for a period of two hours.
- the IPDI transformation rate is 60%.
- Example 6 The procedure is as in Example 6 except that no imidazole is introduced.
- the amounts of catalyst (choline hydrogenocarbonate) are 0.2% and 0.15% by weight.
- the coloring of the reaction medium is evaluated according to the AFNOR NF T20605 or ASTM 01209.84 method.
- the IPDI is redistilled before the trimerization reaction.
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Abstract
Description
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Priority Applications (10)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020007004756A KR100549652B1 (en) | 1997-11-04 | 1998-11-04 | Catalyst and method for trimerization of isocyanates |
AT98954515T ATE251648T1 (en) | 1997-11-04 | 1998-11-04 | CATALYST AND METHOD FOR TRIMERIZING ISOCYANATES |
EP98954515A EP1027380B1 (en) | 1997-11-04 | 1998-11-04 | Catalyst and method for trimerization of isocyanates |
JP2000518997A JP4342723B2 (en) | 1997-11-04 | 1998-11-04 | Catalyst and process for trimerization of isocyanates |
AU11596/99A AU1159699A (en) | 1997-11-04 | 1998-11-04 | Catalyst and method for trimerization of isocyanates |
DE69818857T DE69818857T2 (en) | 1997-11-04 | 1998-11-04 | CATALYST AND METHOD FOR TRIMERIZING ISOCYANATES |
BR9813932-0A BR9813932A (en) | 1997-11-04 | 1998-11-04 | Catalyst and isocyanate trimerization process |
CA002307747A CA2307747A1 (en) | 1997-11-04 | 1998-11-04 | Catalyst and method for trimerization of isocyanates |
US09/530,607 US6635761B1 (en) | 1997-11-04 | 1998-11-04 | Catalyst and method for trimerization of isocyanates |
US10/640,643 US7091341B2 (en) | 1997-11-04 | 2003-08-14 | Catalyst and a method for the trimerization of isocyanates |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR97/13856 | 1997-11-04 | ||
FR9713856A FR2770533B1 (en) | 1997-11-04 | 1997-11-04 | USE OF IMIDAZOLE AS A CO-CATALYST FOR THE TRIMERIZATION OF ISOCYANATES |
FR9713855A FR2770532B1 (en) | 1997-11-04 | 1997-11-04 | ISOCYANATE TRIMERIZATION CATALYST, BASED ON HYDROGENOCARBONATE |
FR97/13855 | 1997-11-04 |
Related Child Applications (2)
Application Number | Title | Priority Date | Filing Date |
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US09530607 A-371-Of-International | 1998-11-04 | ||
US10/640,643 Continuation US7091341B2 (en) | 1997-11-04 | 2003-08-14 | Catalyst and a method for the trimerization of isocyanates |
Publications (1)
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WO1999023128A1 true WO1999023128A1 (en) | 1999-05-14 |
Family
ID=26233919
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PCT/FR1998/002359 WO1999023128A1 (en) | 1997-11-04 | 1998-11-04 | Catalyst and method for trimerization of isocyanates |
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US (2) | US6635761B1 (en) |
EP (2) | EP1375545B1 (en) |
JP (1) | JP4342723B2 (en) |
KR (1) | KR100549652B1 (en) |
CN (1) | CN1184248C (en) |
AT (1) | ATE251648T1 (en) |
AU (1) | AU1159699A (en) |
BR (1) | BR9813932A (en) |
CA (1) | CA2307747A1 (en) |
DE (1) | DE69818857T2 (en) |
WO (1) | WO1999023128A1 (en) |
ZA (1) | ZA9810038B (en) |
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Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3980594A (en) * | 1975-04-23 | 1976-09-14 | The General Tire & Rubber Company | Trimerization of aromatic isocyanates catalyzed by certain ammonium salts |
US4040992A (en) * | 1975-07-29 | 1977-08-09 | Air Products And Chemicals, Inc. | Catalysis of organic isocyanate reactions |
EP0003765A1 (en) * | 1978-02-17 | 1979-09-05 | Bayer Ag | Process for the preparation of isocyanurate groups bearing polyisocyanates based on 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexane and their use as isocyanate component in polyurethane lacquers |
JPS57111310A (en) * | 1980-12-26 | 1982-07-10 | Achilles Corp | Production of rigid foam |
US4542214A (en) * | 1982-03-04 | 1985-09-17 | Air Products And Chemicals, Inc. | Carbamate and carbonate salts of tertiary amines |
EP0351873A2 (en) * | 1988-07-22 | 1990-01-24 | Dainippon Ink And Chemicals, Inc. | Process for the preparation of polyisocyanate |
EP0443167A1 (en) * | 1990-02-23 | 1991-08-28 | Bayer Ag | Trimerization-catalysts, method for their preparation and their use in producing of isocyanate groups containing polyisocyanates |
US5489663A (en) * | 1994-02-17 | 1996-02-06 | Basf Aktiengesellschaft | Preparation of polyisocyanates containing isocyanurate groups and use thereof |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3044261B2 (en) * | 1990-04-11 | 2000-05-22 | 東ソー株式会社 | Method for producing flexible polyurethane foam with excellent air permeability |
CA2052908A1 (en) * | 1990-11-06 | 1992-05-07 | Charles M. Milliren | System for the production of toluene diisocyanate based flexible foams and the flexible foams produced therefrom |
ZA9810038B (en) * | 1997-11-04 | 2000-05-03 | Rhodia Chimie Sa | A catalyst and a method for the trimerization of isocyanates. |
-
1998
- 1998-11-03 ZA ZA9810038A patent/ZA9810038B/en unknown
- 1998-11-04 EP EP03020852.4A patent/EP1375545B1/en not_active Expired - Lifetime
- 1998-11-04 US US09/530,607 patent/US6635761B1/en not_active Expired - Lifetime
- 1998-11-04 BR BR9813932-0A patent/BR9813932A/en not_active IP Right Cessation
- 1998-11-04 EP EP98954515A patent/EP1027380B1/en not_active Expired - Lifetime
- 1998-11-04 AT AT98954515T patent/ATE251648T1/en not_active IP Right Cessation
- 1998-11-04 CA CA002307747A patent/CA2307747A1/en not_active Abandoned
- 1998-11-04 DE DE69818857T patent/DE69818857T2/en not_active Expired - Lifetime
- 1998-11-04 CN CNB988116995A patent/CN1184248C/en not_active Expired - Fee Related
- 1998-11-04 AU AU11596/99A patent/AU1159699A/en not_active Abandoned
- 1998-11-04 WO PCT/FR1998/002359 patent/WO1999023128A1/en active IP Right Grant
- 1998-11-04 JP JP2000518997A patent/JP4342723B2/en not_active Expired - Fee Related
- 1998-11-04 KR KR1020007004756A patent/KR100549652B1/en not_active IP Right Cessation
-
2003
- 2003-08-14 US US10/640,643 patent/US7091341B2/en not_active Expired - Fee Related
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3980594A (en) * | 1975-04-23 | 1976-09-14 | The General Tire & Rubber Company | Trimerization of aromatic isocyanates catalyzed by certain ammonium salts |
US4040992A (en) * | 1975-07-29 | 1977-08-09 | Air Products And Chemicals, Inc. | Catalysis of organic isocyanate reactions |
EP0003765A1 (en) * | 1978-02-17 | 1979-09-05 | Bayer Ag | Process for the preparation of isocyanurate groups bearing polyisocyanates based on 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexane and their use as isocyanate component in polyurethane lacquers |
JPS57111310A (en) * | 1980-12-26 | 1982-07-10 | Achilles Corp | Production of rigid foam |
US4542214A (en) * | 1982-03-04 | 1985-09-17 | Air Products And Chemicals, Inc. | Carbamate and carbonate salts of tertiary amines |
EP0351873A2 (en) * | 1988-07-22 | 1990-01-24 | Dainippon Ink And Chemicals, Inc. | Process for the preparation of polyisocyanate |
EP0443167A1 (en) * | 1990-02-23 | 1991-08-28 | Bayer Ag | Trimerization-catalysts, method for their preparation and their use in producing of isocyanate groups containing polyisocyanates |
US5489663A (en) * | 1994-02-17 | 1996-02-06 | Basf Aktiengesellschaft | Preparation of polyisocyanates containing isocyanurate groups and use thereof |
Non-Patent Citations (1)
Title |
---|
DATABASE WPI Week 8233, Derwent World Patents Index; AN 82-69346e, XP002060412 * |
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JP2003524642A (en) * | 2000-01-20 | 2003-08-19 | ロディア・シミ | Method for obtaining slightly colored branched polyisocyanate and composition obtained |
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Also Published As
Publication number | Publication date |
---|---|
BR9813932A (en) | 2000-09-19 |
DE69818857D1 (en) | 2003-11-13 |
KR20010031693A (en) | 2001-04-16 |
EP1027380B1 (en) | 2003-10-08 |
KR100549652B1 (en) | 2006-02-08 |
ATE251648T1 (en) | 2003-10-15 |
US20050080259A1 (en) | 2005-04-14 |
JP4342723B2 (en) | 2009-10-14 |
DE69818857T2 (en) | 2004-08-19 |
US7091341B2 (en) | 2006-08-15 |
US6635761B1 (en) | 2003-10-21 |
ZA9810038B (en) | 2000-05-03 |
JP2001521952A (en) | 2001-11-13 |
CN1184248C (en) | 2005-01-12 |
AU1159699A (en) | 1999-05-24 |
EP1375545B1 (en) | 2016-06-29 |
EP1375545A1 (en) | 2004-01-02 |
CN1280588A (en) | 2001-01-17 |
CA2307747A1 (en) | 1999-05-14 |
EP1027380A1 (en) | 2000-08-16 |
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